Polyolefin graft copolymers made with fluorinated monomers

ABSTRACT

A fluorine-containing graft copolymer is made from a backbone of an olefin polymer material to which is graft polymerized (a) at least one gaseous fluorinated monomer such as vinylidene fluoride, (b) at least one fluorinated acrylic acid or ester, (c) a mixture of (a) and (b), or (d) a mixture of (a) and/or (b) and a non-fluorinated monomer such as methyl methacrylate. An organic peroxide or a polymeric peroxide is used as the initiator for the graft polymerization process. The graft copolymers have improved surface properties and oxygen barrier properties, and improved thermal stability.

This application is a divisional of application Ser. No. 09/364,444,filed on Jul. 30, 1999, now U.S. Pat. No. 6,337,373, issued on Jan. 8,2002.

FIELD OF THE INVENTION

This invention relates to polyolefin graft copolymers.

BACKGROUND OF THE INVENTION

Polyolefins are relatively inexpensive and are superior inprocessability, toughness, water resistance, organic solvent resistance,and chemical resistance. However, they lack stability toward anoxidizing environment and are deficient in surface properties such ascoefficient of friction and scratch and mar resistance, as well as inoxygen barrier properties.

Fluorinated polymers are characterized by resistance to harsh chemicalsas well as stability toward heat, ultraviolet light, high energyradiation, and oxidation. Polyvinylidene fluoride, a member of the classof fluorinated polymers, is a semi-crystalline material with a highdielectric constant that can easily be processed on conventional moldingand extrusion equipment. It also has high mechanical and impactstrength, and high resistance to creep, fatigue and abrasion. Film madefrom this polymer has excellent oxygen and moisture barrier properties.

Graft copolymers of polyolefins are of interest because they are capableof possessing some properties of the polymerized grafting monomer aswell as of the polyolefin backbone.

U.S. Pat. Nos. 4,806,581 and 4,605,704 disclose a process for makinggraft copolymers in which liquid monomer and initiator are absorbed intosolid polyolefin particles, followed by reaction of the monomer in theparticles to produce polymer and graft copolymer simultaneously in thesame reactor. The grafting monomers include vinyl monohalides, such asvinyl chloride, and dihalides, such as vinylidene fluoride, which can bemixed with less than 50% of another monomer such as an acrylate ormethacrylate ester. The resulting product can be molded to formtransparent or translucent molded articles.

There is still a need for an improved process for producing graftcopolymers comprising a polyolefin backbone which are useful for formingarticles with improved surface and barrier properties as well asimproved thermal stability.

SUMMARY OF THE INVENTION

In one embodiment of this invention, a fluorine-containing graftcopolymer comprises a backbone of an olefin polymer material to which isgraft polymerized (a) at least one fluorinated gaseous monomer havingthe formula CR₁R₂═CR₃R₄, where R₁=H, F, or Cl; R₂=H, F, or Cl; R₃=H, F,CH₃, CF₃, or Cl, and R₄=H, F, or Cl, wherein at least two fluorine atomsare present, and, optionally, (b) at least one non-fluorinated monomerselected from the group consisting of (i) vinyl-substituted aromatic,heterocyclic, and alicyclic compounds, (ii) unsaturated aliphaticnitrites, and (iii) unsaturated aliphatic monocarboxylic acids or estersthereof, wherein the total amount of monomers added is about 1 to about100 parts per hundred parts of the olefin polymer material, and theparticulate olefin polymer material has a weight average diameter ofabout 0.4-7 mm, a surface area of at least 0.1 m²/g, and a pore volumefraction of at least about 0.07, and wherein more than 40% of the poresin the particle have a diameter greater than 1 micron.

This graft copolymer is prepared by a process comprising, in anon-oxidizing atmosphere:

(1) treating a particulate olefin polymer material at a temperature ofabout 10° to about 70° C. with about 0.1 to about 6.0 parts per hundredparts of the olefin polymer material, of an organic compound that is achemical free radical polymerization initiator and has a decompositionhalf-life at the temperature used in step (2) of about 1 to about 240minutes,

(2) increasing the temperature to about 60° to about 115° C.,

(3) adding (a) at least one fluorinated gaseous monomer having theformula CR₁R₂═CR₃R₄, where R₁=H, F, or Cl; R₂=H, F, or Cl; R₃=H, F, CH₃,CF₃, or Cl, and R₄=H, F, or Cl, wherein at least two fluorine atoms arepresent, and, optionally, (b) at least one non-fluorinated monomerselected from the group consisting of (i) vinyl-substituted aromatic,heterocyclic, and alicyclic compounds, (ii) unsaturated aliphaticnitrites, and (iii) unsaturated aliphatic monocarboxylic acids or estersthereof, wherein the total amount of monomers added is about 1 to about100 parts per hundred parts of the olefin polymer material, to produceand maintain a pressure of about 200 to about 900 psi

(4) heating at a temperature within the range specified in step (2) forabout 1 to about 6 hours,

(5) cooling to room temperature, and

(6) releasing the pressure to remove unreacted monomer,

wherein the particulate olefin polymer material has a weight averagediameter of about 0.4-7 mm, a surface area of at least 0.1 m²/g, and apore volume fraction of at least about 0.07 and wherein more than 40% ofthe pores in the particle have a diameter greater than 1 micron.

In another embodiment, a fluorine-containing graft copolymer is preparedin a non-oxidizing environment by:

(1) heating a peroxidized olefin polymer material to a temperature ofabout 60° to about 140° C.,

(2) adding (a) at least one fluorinated gaseous monomer having theformula CR₁R₂═CR₃R₄, where R₁=H, F, or Cl; R₂=H, F, or Cl; R₃=H, F, CH₃,CF₃, or Cl, and R₄=H, F, or Cl, wherein at least two fluorine atoms arepresent, and, optionally, (b) at least one non-fluorinated monomerselected from the group consisting of (i) vinyl-substituted aromatic,heterocyclic, and alicyclic compounds, (ii) unsaturated aliphaticnitriles, and (iii) unsaturated aliphatic monocarboxylic acids or estersthereof, wherein the total amount of monomers added is about 1 to about100 parts per hundred parts of the olefin polymer material, to produceand maintain a pressure of about 200 to about 900 psi

(3) heating at a temperature within the range specified in step (1) forabout 1 to about 6 hours,

(4) cooling to room temperature, and

(5) releasing the pressure to remove unreacted monomer.

Another embodiment of this invention comprises a fluorine-containinggraft copolymer comprising an olefin polymer backbone to which is graftpolymerized about 1 to about 120 parts per hundred parts of the olefinpolymer material, of (a) at least one fluorinated monomer having theformula CH₂═C(R₁)—(COOR₂), where R₁=H, CH₃, or CF₃, and R₂ is H or apartially or completely fluorinated C₁-C₁₂ alkyl group, and, optionally,(b) at least one non-fluorinated monomer selected from the groupconsisting of (i) vinyl-substituted aromatic, heterocyclic, andalicyclic compounds, (ii) unsaturated aliphatic nitrites, and (iii)unsaturated aliphatic monocarboxylic acids or esters thereof.

This graft copolymer is prepared by a process comprising, in anon-oxidizing atmosphere:

(1) treating a particulate olefin polymer material at a temperature ofabout 60° C. to about 125° C. with about 0.1 to about 6.0 parts perhundred parts of the olefin polymer material, of an organic compoundthat is a chemical free radical polymerization initiator and has adecomposition half-life at the temperature used of about 1 to about 240minutes;

(2) treating the olefin polymer material at the temperature selectedover a time period that coincides with or following (1), with or withoutoverlap, with (a) at least one fluorine-containing monomer having theformula CH₂═C(R₁)—(COOR₂), where R₁=H, CH₃, or CF₃, and R₂ is H or apartially or completely fluorinated C₁-C₁₂ alkyl group, and, optionally,(b) at least one non-fluorinated monomer selected from the groupconsisting of (i) vinyl-substituted aromatic, heterocyclic, andalicyclic compounds, (ii) unsaturated aliphatic nitrites, and (iii)unsaturated aliphatic monocarboxylic acids or esters thereof, whereinthe total amount of monomers added is about 1 to about 120 parts perhundred parts of the olefin polymer material, the monomer being added tothe olefin polymer material over a time period from 5 minutes to 3-4hours to provide a rate of addition that is less than about 4.5 pph perminute at any addition level; and thereafter

(3) simultaneously or successively, in any order, removing any unreactedmonomer from the resulting grafted particulate olefin polymer material,and decomposing any unreacted initiator and deactivating any residualfree radicals in the material.

Another embodiment of the invention is a fluorine-containing graftcopolymer comprising a backbone of an olefin polymer material to whichis graft polymerized a combination of:

(a) at least one fluorinated gaseous monomer having the formulaCR₁R₂═CR₃R₄, where R₁=H, F, or Cl; R₂=H, F, or Cl; R₃=H, F, CH₃, CF₃, orCl, and R₄=H, F, or Cl, wherein at least two fluorine atoms are present,

(b) at least one fluorinated monomer having the formulaCH₂═C(R₁)—(COOR₂), where R₁=H, CH₃, or CF₃, and R₂ is H or a partiallyor completely fluorinated C₁-C₁₂ alkyl group, and, optionally,

(c) at least one non-fluorinated monomer selected from the groupconsisting of (i) vinyl-substituted aromatic, heterocyclic, andalicyclic compounds, (ii) unsaturated aliphatic nitrites, and (iii)unsaturated aliphatic monocarboxylic acids or esters thereof,

wherein the total amount of polymerized monomers is about 1 to about 100parts per hundred parts of the olefin polymer material.

This graft copolymer is prepared in a non-oxidizing environment by:

(1) treating a particulate olefin polymer material at a temperature ofabout 10° to about 70° C. with about 0.1 to about 6.0 parts per hundredparts of the propylene polymer material, of an organic compound that isa chemical free radical polymerization initiator and has a decompositionhalf-life at the temperature used in step (2) of about 1 to about 240minutes,

(2) increasing the temperature to about 60° to about 115° C.,

(3) adding a combination of:

(a) at least one fluorinated gaseous monomer having the formulaR₁R₂═CR₃R₄, where R₁=H, F, or Cl; R₂=H, F, or Cl; R₃=H, F, CH₃, CF₃, orCl and R₄=H, F, or Cl, wherein at least two fluorine atoms are present,to produce and maintain a pressure of about 200 to about 900 psi,

(b) at least one fluorinated monomer having the formulaCH₂═C(R₁)—(COOR₂), where R₁=H, CH₃, or CF₃, and R₂ is H or a partiallyor completely fluorinated C₁-C₁₂ alkyl group, and, optionally,

(c) at least one non-fluorinated monomer selected from the groupconsisting of (i) vinyl-substituted aromatic, heterocyclic, andalicyclic compounds, (ii) unsaturated aliphatic nitrites, and (iii)unsaturated aliphatic monocarboxylic acids or esters thereof,

wherein the total amount of monomers added is about 1 to about 100 partsper hundred parts of the olefin polymer material,

(4) heating at a temperature within the range specified in step (2) forabout 1 to about 6 hours,

(5) cooling to room temperature, and

(6) releasing the pressure to remove unreacted monomer.

The graft polymerized fluorine-containing monomers are found at thesurface of articles made from the graft copolymers of this invention aswell as in the inside of the article, thereby reducing the coefficientof friction and improving scratch and mar resistance and oxygen barrierproperties. The thermal oxidative stability of the polymer is alsoimproved by the presence of the polymerized fluorinated monomers.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a plot of temperature (° C.) against the % of the originalweight of the polymer and shows the weight loss during thermogravimetricanalysis in air and therefore the thermal oxidative stability of thepolymers. The grafted polymers comprise a backbone of propylenehomopolymer, to which was grafted poly(vinylidene fluoride) orpoly(vinylidene fluoride/methyl methacrylate).

DETAILED DESCRIPTION OF THE INVENTION

In a first embodiment, the fluorine-containing graft copolymer of thisinvention comprises a backbone of an olefin polymer material, to whichis graft polymerized (a) at least one fluorinated gaseous monomer havingthe formula CR₁R₂═CR₃R₄, where R₁=H, F, or Cl; R₂=H, F, or Cl; R₃=H, F,CH₃, CF₃, or Cl, and R₄=H, F, or Cl, wherein at least two fluorine atomsare present, and, optionally, (b) at least one non-fluorinated monomerselected from the group consisting of (i) vinyl-substituted aromatic,heterocyclic, and alicyclic compounds, (ii) unsaturated aliphaticnitriles, and (iii) unsaturated aliphatic monocarboxylic acids or estersthereof. The polymerizable monomers are present in a total amount ofabout 1 to about 100 parts per hundred parts of the olefin polymermaterial, preferably about 5 to about 50 parts.

A gaseous monomer is one which is a gas at a temperature above 0° C. atatmospheric pressure.

When the grafting monomer is a gaseous monomer, either alone or incombination with a non-fluorinated monomer, the olefin polymer materialthat is used as the backbone of the graft copolymer is selected from thegroup consisting of:

(1) a homopolymer of a linear or branched C₂₋₈ alpha-olefin;

(2) a random copolymer of a linear or branched C₂₋₈ alpha-olefin with adifferent olefin selected from the group consisting of C₂₋₁₀alpha-olefins, provided that, when the different olefin is ethylene, themaximum polymerized ethylene content is about 10% by weight; when theolefin is propylene and the different olefin is a C₄₋₁₀ alpha-olefin,the maximum polymerized content thereof is 20% by weight; and when theolefin is ethylene and the different olefin is a C₃₋₁₀ alpha-olefin, themaximum polymerized content thereof is 10% by weight;

(3) a random terpolymer of a linear or branched C₃₋₈ alpha-olefin andtwo different olefins selected from the group consisting of ethylene andC₄₋₈ alpha-olefins, provided that the maximum polymerized content of thedifferent C₄₋₈ alpha-olefins is 20% by weight, and when ethylene is oneof the different olefins, the maximum polymerized ethylene content is 5%by weight, and

(4) linear low density polyethylene comprising a copolymer of ethyleneand about 0.5% to about 35%, preferably about 1% to about 20%, and mostpreferably about 2% to about 15%, of at least one C₃-C₁₂ alpha-olefin,preferably a C₄-C₈ alpha-olefin, and most preferably 1-octene, having adensity of about 0.88 g/cm³ to about 0.935 g/cm³, preferably about 0.90g/cm³ to about 0.925 g/cm³.

The olefin polymer material used as the backbone of the graft copolymeris in particulate form and has a weight average diameter of about 0.4-7mm, a surface area of at least 0.1 m²/g, and a pore volume fraction ofat least about 0.07, i.e., seven percent of the volume is pores, andwherein more than 40% of the pores in the particle have a diametergreater than 1 micron. Preferably more than 50% of the pores in theparticle have a diameter greater than 1 micron, and most preferably morethan 90% of the pores in the particle have a diameter greater than 1micron. The pore volume fraction is preferably at least 0.12, mostpreferably at least 0.20.

Examples of suitable gaseous monomers include vinylidene fluoride,hexafluoropropylene, tetrafluoroethylene, 1-chloro-1-fluoroethylene, andchlorotrifluoroethylene.

The non-fluorinated monomers that can be present in addition to thefluorinated gaseous monomer include any monomeric vinyl compound capableof being polymerized by free radicals, wherein the vinyl radicalH₂C═CR—, in which R=H or methyl, is attached to a straight or branchedaliphatic chain or to a substituted or unsubstituted aromatic,heterocyclic, or alicyclic ring in a mono- or polycyclic compound.Typical substituent groups can be alkyl, hydroxyalkyl, aryl, and halo.Usually the vinyl monomer will be a member of one of the followingclasses: (1) vinyl-substituted aromatic, heterocyclic, or alicycliccompounds, including styrene, vinylnaphthalene, vinylpyridine,vinylpyrrolidone, vinylcarbazole, and homologs thereof, e.g., alpha- andpara-methylstyrene, methylchlorostyrene, p-tert-butylstyrene,methylvinylpyridine, and ethylvinylpyridine, and (2) unsaturatedaliphatic nitriles and carboxylic acids and their esters includingacrylonitrile; methacrylonitrile; acrylic acid; acrylate esters such asthe methyl ethyl, hydroxyethyl, 2-ethylhexyl, and butyl acrylate esters;methacrylic acid; ethacrylic acid; methacrylate esters, such as themethyl, ethyl, butyl, benzyl, phenylethyl, phenoxyethyl, epoxypropyl,and hydroxpropyl methacrylate esters. Multiple monomers from the same ordifferent classes can be employed. The preferred non-fluorinatedmonomers are styrenic and acrylic monomers.

The process for making the graft copolymers of this invention using atleast one gaseous fluorinated monomer, or a combination of a gaseousfluorinated monomer and at least one non-fluorinated monomer comprises,in a non-oxidizing environment,

(1) treating a particulate olefin polymer material at a temperature ofabout 10° to 70° C. with about 0.1 to about 6.0 parts per hundred partsof the olefin polymer material, of an organic compound that is achemical free radical polymerization initiator and has a decompositionhalf-life at the temperature used in step (2) of about 1 to about 240minutes;

(2) increasing the temperature to about 60° to about 115° C.,

(3) adding (a) at least one fluorinated gaseous monomer having theformula CR₁R₂═CR₃R₄, where R₁=H, F, or Cl; R₂=H, F, or Cl; R₃=H, F, CH₃,CF₃, or Cl, and R₄=H, F, or Cl, wherein at least two fluorine atoms arepresent, and, optionally, (b) at least one non-fluorinated monomerselected from the group consisting of (i) vinyl-substituted aromatic,heterocyclic, and alicyclic compounds, (ii) unsaturated aliphaticnitriles, and (iii) unsaturated aliphatic monocarboxylic acids or estersthereof, wherein the total amount of monomer added is about 1 to about100 parts, preferably about 5 to about 50 parts, per hundred parts ofthe olefin polymer material, to produce and maintain a pressure of about200 to about 900 psi, preferably about 250 to about 400 psi,

(4) heating at a temperature withing the range specified in step (2) forabout 1 to about 6 hours,

(5) cooling to room temperature, and

(6) releasing the pressure to remove unreacted monomer,

wherein the particulate olefin polymer material has a weight averagediameter of about 0.4-7 mm, a surface area of at least 0.1 m/²g, and apore volume fraction of at least about 0.07, and wherein more than 40%of the pores in the particle, preferably more than 50%, and mostpreferably more than 90%, have a diameter greater than 1 micron.

According to the method of the invention, free radical or active sitesare produced in the particulate olefin polymer material by treating thepolymer material with an organic compound that is a free-radicalgenerating polymerization initiator and has a decomposition half-life atthe temperature employed of about 1 to about 240, preferably about 5 toabout 100, and most preferably about 10 to about 40, minutes. Organicperoxides, and especially those that generate alkoxy radicals,constitute the preferred class of initiators. These include acylperoxides, such as benzoyl and dibenzoyl peroxides; dialkyl and aralkylperoxides, such as di-tert-butyl peroxide, dicumyl peroxide, cumyl butylperoxide, 1,1-di-tert-butylperoxy-3,5,5-trimethylcyclohexane,2,5-dimethyl-2,5-di-tert-butylperoxyhexane, and bis(alpha-tert-butylperoxyisopropylbenzene); peroxy esters, such astert-butylperoxypivalate, tert-butyl perbenzoate, tert-butyl peroctoate;2,5-dimethylhexyl 2,5-di(perbenzoate), tert-butyl di(perphthalate),tert-butylperoxy-2-ethyl hexanoate; and1,1-dimethyl-3-hydroxybutylperoxy-2-ethyl hexanoate; and peroxycarbonates, such as di(2-ethylhexyl) peroxy dicarbonate,di(n-propyl)peroxy dicarbonate, and di(4-tert-butylcyclohexyl)peroxydicarbonate. Polymeric peroxides such as peroxidized propylenehomopolymers, copolymers, and terpolymers can also be used as theinitiator. Peroxy esters, peroxy carbonates, and polymeric peroxides arepreferred. Peroxy carbonates are most preferred. Use of a polymericperoxide as an initiator will be described in more detail below.

“Non-oxidizing environment” is the environment or atmosphere to whichthe olefin polymer material is exposed during the preparation of thegraft copolymer and means an environment in which the active oxygenconcentration, i.e., the concentration of oxygen in a form that willreact with the free radicals in the polymer material, is less than 15%,preferably less than 5%, and most preferably less than 1% by volume. Themost preferred concentration of active oxygen is 0.004% or lower byvolume. Within these limits, the non-oxidizing atmosphere can be anygas, or mixture of gases, that is oxidatively inert toward the freeradicals in the olefin polymer material, e.g., nitrogen, argon, helium,and carbon dioxide.

A fluorinated solvent such as 2,2-dichloro-1,1,1-trifluoroethane, methylnonafluorobutyl ether, or methyl nonafluoroisobutyl ether is preferablyused when the fluorinated monomer is a gas, or a mixture of afluorinated gaseous monomer and a liquid monomer. The fluorinatedsolvent solubilizes the monomer so that more polymerized monomer isincorporated into the graft copolymer.

In another embodiment, the fluorine-containing graft copolymer of thisinvention comprises an olefin polymer backbone to which is graftpolymerized (a) at least one fluorinated acrylic or methacrylic monomerhaving the formula CH₂═C(R₁)—(COOR₂) where R₁=H, CH₃, or CF₃, and R₂ isH or a partially or completely fluorinated C₁₋₁₂ alkyl group, and,optionally, (b) at least one non-fluorinated monomer selected from thegroup consisting of (i) vinyl-substituted aromatic, heterocyclic, andalicyclic compounds, (ii) unsaturated aliphatic nitrites, and (iii)unsaturated aliphatic monocarboxylic acids or esters thereof.

The fluorinated acrylic and methacrylic monomers are liquids at atemperature above 0° C. at atmospheric pressure. The monomers arepresent in a total amount of about 1 to about 120 parts, preferablyabout 2 to about 60 parts, and most preferably about 5 to about 40 partsper hundred parts of the olefin polymer material.

Examples of suitable fluorinated acrylic and methacrylic monomersinclude 2,2,3,4,4,4-hexafluorobutyl methacrylate;2,2,3,3,4,4,4-heptafluorobutyl acrylate; 2,2,3,3,4,4-hexafluorobutylacrylate; 2,2,2-trifluoroethyl acrylate;2,2,3,3,4,4,5,5,5-nonafluoropentyl acrylate;3,3,4,4,5,5,6,6,6-nonafluorohexyl methacrylate;2,2,3,3,3-pentafluoropropyl acrylate;2,2,3,3,4,4,5,5,6,6,6-undecafluorohexyl acrylate;1,1,1,2,2,2-hexafluororprop-2-yl acrylate;3,3,4,4,5,5,6,6,7,7,8,8,9,9,10,10,10-heptadecafluorodecyl acrylate,2-(trifluoromethyl) acrylic acid; 2,2,3,3-tetrafluoropropyl acrylate;2,2,3,3-tetrafluoropropyl methacrylate; 1,1,1,3,3,3-hexafluoroisopropylmethacrylate, and 2,2,3,3,4,4,5,5-octafluoropentyl methacrylate.

When the grafting monomer is a fluorinated acrylic or methacrylicmonomer described above, or a mixture of a fluorinated gaseous monomerand a fluorinated acrylic or methacrylic monomer, with or without anon-fluorinated monomer, the olefin polymer material that is used as thebackbone of the graft copolymer can be:

(1) a homopolymer of propylene having an isotactic index greater than80, preferably about 85 to about 99;

(2) a copolymer of propylene and an olefin selected from the groupconsisting of ethylene and 4-10 C alpha-olefins, provided that when theolefin is ethylene, the maximum polymerized ethylene content is 10%,preferably about 4%, and when the olefin is a 4-10 C alpha-olefin, themaximum polymerized content thereof is 20% by weight, preferably about16%, the copolymer having an isotactic index greater than 85;

(3) a terpolymer of propylene and two olefins selected from the groupconsisting of ethylene and 4-8 C alpha-olefins, provided that themaximum polymerized 4-8 C alpha-olefin content is 20% by weight,preferably about 16%, and, when ethylene is one of the olefins, themaximum polymerized ethylene content is 5% by weight, preferably about4%, the terpolymer having an isotactic index greater than 85;

(4) an olefin polymer composition comprising:

(a) about 10% to about 60% by weight, preferably about 15% to about 55%,of a propylene homopolymer having an isotactic index greater than 80,preferably about 85 to about 98, or a copolymer of monomers selectedfrom the group consisting of (i) propylene and ethylene, (ii) propylene,ethylene and a 4-8 C alpha-olefin, and (iii) propylene and a 4-8 Calpha-olefin, the copolymer having a polymerized propylene content ofmore than 85% by weight, preferably about 90% to about 99%, and anisotactic index greater than 85;

(b) about 5% to about 25% by weight, preferably about 5% to about 20%,of a copolymer of ethylene and propylene or a 4-8 C alpha-olefin that isinsoluble in xylene at ambient temperature; and

(c) about 30% to about 70% by weight, preferably about 40% to about 65%,of an elastomeric copolymer of monomers selected from the groupconsisting of (i) ethylene and propylene, (ii) ethylene, propylene, anda 4-8 C alpha-olefin, and (iii) ethylene and a 4-8 C alpha-olefin, thecopolymer optionally containing about 0.5% to about 10% by weight of apolymerized diene and containing less than 70% by weight, preferablyabout 10% to about 60%, most preferably about 12% to about 55%, ofpolymerized ethylene and being soluble in xylene at ambient temperatureand having an intrinsic viscosity, measured in decahydronaphthalene at135° C., of about 1.5 to about 4.0 dl/g,

wherein the total amount of (b) and (c), based on the total olefinpolymer composition, is about 50% to about 90%, the weight ratio of(b)/(c) is less than 0.4, preferably 0.1 to 0.3, and the composition isprepared by polymerization in at least two stages and has a flexuralmodulus of less than 150 MPa; or

(5) a thermoplastic olefin comprising:

(a) about 10% to about 60%, preferably about 20% to about 50%, of apropylene homopolymer having an isotactic index greater than 80, or acopolymer of monomers selected from the group consisting of (i) ethyleneand propylene, (ii) ethylene, propylene and a 4-8 C alpha-olefin, and(iii) ethylene and a 4-8 C alpha-olefin, the copolymer having apolymerized propylene content greater than 85% and an isotactic index ofgreater than 85;

(b) about 20% to about 60%, preferably about 30% to about 50%, of anamorphous copolymer from monomers selected from the group consisting of(i) ethylene and propylene, (ii) ethylene, propylene, and a 4-8 Calpha-olefin, and (iii) ethylene and a 4-8 C alpha-olefin, the copolymeroptionally containing about 0.5% to about 10% of a polymerized diene,and containing less than 70% polymerized ethylene and being soluble inxylene at ambient temperature; and

(c) about 3% to about 40%, preferably about 10% to about 20%, of acopolymer of ethylene and propylene or a 4-8 C alpha-olefin that isinsoluble in xylene at ambient temperature,

wherein the thermoplastic olefin has a flexural modulus of greater than150 but less than 1200 MPa, preferably about 200 to about 1100 MPa, andmost preferably about 200 to about 1000 MPa.

Room or ambient temperature is ˜25° C.

The 4-8 C alpha-olefins useful in the preparation of (4) and (5)include, for example, butene-1, pentene-1; hexene-1; 4-methyl-1-pentene,and octene-1.

The diene, when present, is typically a butadiene; 1,4-hexadiene;1,5-hexadiene, or ethylidenenorbornene.

Propylene polymer materials (4) and (5) can be prepared bypolymerization in at least two stages, where in the first stage thepropylene; propylene and ethylene; propylene and an alpha-olefin, orpropylene, ethylene and an alpha-olefin are polymerized to formcomponent (a) of (4) or (5), and in the following stages the mixtures ofethylene and propylene; ethylene and the alpha-olefin, or ethylene,propylene and the alpha-olefin, and optionally a diene, are polymerizedin the presence of (a) to form components (b) and (c) of (4) or (5).

The polymerization can be conducted in liquid phase, gas phase, orliquid-gas phase using separate reactors, all of which can be doneeither by batch or continuously. For example, it is possible to carryout the polymerization of component (a) using liquid propylene as adiluent, and the polymerization of components (b) and (c) in gas phase,without intermediate stages except for the partial degassing of thepropylene. All gas phase is the preferred method.

The preparation of propylene polymer material (4) is described in moredetail in U.S. Pat. Nos. 5,212,246 and 5,409,992, which are incorporatedherein by reference. The preparation of propylene polymer material (5)is described in more detail in U.S. Pat. Nos. 5,302,454 and 5,409,992,which are incorporated herein by reference.

Propylene homopolymer is the preferred propylene polymer backbonematerial. A porous olefin polymer material such as those described abovecan also be used for the backbone polymer.

The process for making the graft copolymers of this invention using atleast one fluorinated acrylic or methacrylic monomer, with or without anon-fluorinated monomer, comprises, in a non-oxidizing environment:

(1) treating a particulate olefin polymer material at a temperature ofabout 60° C. to about 125° C., preferably about 80°-120° C., with about0.1 to about 6.0 parts per hundred parts of the olefin polymer material,of an organic compound that is a chemical free radical polymerizationinitiator and has a decomposition half-life at the temperature used ofabout 1 to about 240 minutes;

(2) treating the olefin polymer material at the temperature selectedover a time period that coincides with or follows (1), with or withoutoverlap, with (a) at least one fluorinated monomer having the formulaCH₂═C(R₁)—(COOR₂), where R₁=H, CF₃, or CH₃ and R₂ is H or a partially orcompletely fluorinated C₁-C₁₂ alkyl group, and, optionally, (b) at leastone non-fluorinated monomer selected from the group consisting of (i)vinyl-substituted aromatic, heterocyclic, and alicyclic compounds, (ii)unsaturated aliphatic nitrites, and (iii) unsaturated aliphaticmonocarboxylic acids or esters thereof, wherein the total amount ofmonomer added is about 1 to about 120 parts, preferably about 2 to about60 parts, and most preferably about 5 to about 40 parts, per hundredparts of the olefin polymer material, the monomer being added to saidolefin polymer material over a time period from 5 minutes to 3-4 hoursto provide a rate of addition that is less than about 4.5 pph per minuteat any addition level; and thereafter

(3) simultaneously or successively, in any order, removing any unreactedgrafting monomer from the resulting grafted particulate olefin polymermaterial, and decomposing any unreacted initiator and deactivating anyresidual free radicals in said material.

Preparation of graft copolymers by contacting an olefin polymer materialwith a free radical polymerization initiator such as an organicperoxide, and a vinyl monomer is described in more detail in U.S. Pat.No. 5,104,074, which is incorporated herein by reference.

A peroxidized propylene polymer material can also be used for making thefluorine-containing graft copolymers of this invention. The startingmaterial for making the peroxidized polymer can be:

(1) a homopolymer of propylene having an isotactic index greater than80, preferably about 85 to about 99;

(2) a copolymer of propylene and an olefin selected from the groupconsisting of ethylene and 4-10 C alpha-olefins, provided that when theolefin is ethylene, the maximum polymerized ethylene content is 10%,preferably about 4%, and when the olefin is a 4-10 C alpha-olefin, themaximum polymerized content thereof is 20% by weight, preferably about16%, the copolymer having an isotactic index greater than 85;

(3) a terpolymer of propylene and two olefins selected from the groupconsisting of ethylene and 4-8 C alpha-olefins, provided that themaximum polymerized 4-8 C alpha-olefin content is 20% by weight,preferably about 16%, and, when ethylene is one of the olefins, themaximum polymerized ethylene content is 5% by weight, preferably about4%, the terpolymer having an isotactic index greater than 85;

A porous propylene homopolymer, copolymer, or terpolymer such as thosedescribed above can also be used as the backbone polymer.

The starting polymer is irradiated under an electron beam at a dose rateof 0.2-10 Mrad in an inert atmosphere. The irradiated polymer is thentreated with oxygen at a concentration of greater than 0.004% but lessthan 15% by volume, preferably less than 8%, and most preferably lessthan 3%, at a temperature of about 40° to about 110° C., preferablyabout 80° C., and then at a temperature of at least 110° C. up to thesoftening point of the polymer (140° C. for a propylene homopolymer).The total reaction time is typically up to three hours. After the oxygentreatment, the polymer is treated at 140° C. for one hour in an inertatmosphere such as nitrogen to quench any active free radicals.

The process for making the graft copolymers of this invention using aperoxidized olefin polymer material comprises, in a non-oxidizingenvironment:

(1) heating a peroxidized olefin polymer material to a temperature ofabout 60° to about 140° C.,

(2) adding (a) at least one fluorinated gaseous monomer having theformula CR₁R₂═CR₃R₄, where R₁=H, F, or Cl; R₂=H, F, or Cl; R₃=H, F, CH₃,CF₃, or Cl, and R₄=H, F, or Cl, wherein at least two fluorine atoms arepresent, and, optionally, (b) at least one non-fluorinated monomerselected from the group consisting of (i) vinyl-substituted aromatic,heterocyclic, and alicyclic compounds, (ii) unsaturated aliphaticnitrites, and (iii) unsaturated aliphatic monocarboxylic acids or estersthereof, wherein the total amount of monomer added is about 1 to about100 parts, preferably about 5 to about 50 parts, per hundred parts ofthe olefin polymer material, to produce and maintain a pressure of about200 to about 900 psi preferably about 250 to about 400 psi,

(3) heating at a temperature within the range specified in step (1) forabout 1 to about 6 hours,

(4) cooling to room temperature, and

(5) releasing the pressure to remove unreacted monomer.

The peroxidized olefin polymer material can also be used in thepreparation of the graft copolymers of this invention when at least onefluorinated monomer having the formula CH₂═C(R₁)—(COOR₂), where R₁=H,CH₃, or CF₃, and R₂ is H or a partially or completely fluorinated C₁-C₁₂alkyl group, or a mixture of this monomer and at least one fluorinatedgaseous monomer, with or without a non-fluorinated monomer, is used asthe grafting monomer.

In another embodiment, the fluorine-containing graft copolymer of thisinvention comprises a backbone of an olefin polymer material, to whichis graft polymerized a combination of:

(a) at least one fluorinated gaseous monomer having the formulaCR₁R₂═CR₃R₄, where R₁=H, F, or Cl; R₂=H, F, or Cl; R₃=H, F, CH₃, CF₃, orCl, and R₄=H, F, or Cl, wherein at least two fluorine atoms are present,

(b) at least one fluorinated monomer having the formulaCH₂═C(R₁)—(COOR₂), where R₁=H, CH₃, or CF₃, and R₂ is H or a partiallyor completely fluorinated C₁-C₁₂ alkyl group, and, optionally,

(c) at least one non-fluorinated monomer selected from the groupconsisting of (i) vinyl-substituted aromatic, heterocyclic, andalicyclic compounds, (ii) unsaturated aliphatic nitrites, and (iii)unsaturated aliphatic monocarboxylic acids or esters thereof.

The polymerized monomers are present in a total amount of about 1 toabout 100 parts, preferably about 5 to about 50 parts, per hundred partsof the olefin polymer material.

The olefin polymer material used as the backbone of these graftcopolymers can be any one of the materials described in connection withthe graft copolymers made with the fluorinated acrylic or methacrylicmonomers. A porous olefin polymer material such as those described abovecan also be used as the backbone polymer.

The process for making this graft copolymer comprises, in anon-oxidizing environment:

(1) treating a particulate olefin polymer material at a temperature ofabout 10° to about 70° C. with about 0.1 to about 6.0 parts per hundredparts of the olefin polymer material, of an organic compound that is achemical free radical polymerization initiator and has a decompositionhalf-life at the temperature used in step (2) of about 1 to about 240minutes,

(2) increasing the temperature to about 60° to about 115° C.,

(3) adding a combination of:

(a) at least one fluorinated gaseous monomer having the formulaR₁R₂═CR₃R₄, where R₁=H, F, or Cl; R₂=H, F, or Cl; R₃=H, F, CH₃, CF₃, orCl, and R₄=H, F, or Cl, wherein at least two fluorine atoms are present,to produce and maintain a pressure of about 200 to about 900 psipreferably about 250 to about 400 psi,

(b) at least one fluorinated monomer having the formulaCH₂═C(R₁)—(COOR₂), where R₁=H, CH₃, or CF₃, and R₂ is H or a partiallyor completely fluorinated C₁-C₁₂ alkyl group, and, optionally,

(c) at least one non-fluorinated monomer selected from the groupconsisting of (i) vinyl-substituted aromatic, heterocyclic, andalicyclic compounds, (ii) unsaturated aliphatic nitrites, and (iii)unsaturated aliphatic monocarboxylic acids or esters thereof,

wherein the total amount of monomers added is about 1 to about 100parts, preferably about 5 to about 50 parts, per hundred parts of theolefin polymer material,

(4) heating at a temperature within the range specified in step (2) forabout 1 hour to about 6 hours,

(5) cooling to room temperature, and

(6) releasing the pressure to remove unreacted monomer.

In this process, the free radical polymerization initiator is addedfirst, and then either (a) the fluorinated acrylic or methacrylicmonomer and the fluorinated gaseous monomer are sequentially polymerizedaccording to the processes described above, in any order, or (b) thefluorinated acrylic or methacrylic monomer and the fluorinated gaseousmonomer are simultaneously polymerized according to the processdescribed above for gaseous monomers. The pressure in the reactor isthen released, and the reactor is purged with an inert gas such asnitrogen to remove unreacted monomer.

When the sequential polymerization process is used, if thepolymerization time of the first monomer exceeds 10-15 times thehalf-life of the initiator, a second portion of the initiator is addedbefore adding the second monomer. If a gaseous monomer is polymerizedfirst, the pressure in the reactor is released prior to adding thesecond monomer.

Other additives such as pigments, nucleating agents, pigment dispersingaids, slip agents, and fillers such as talc, calcium carbonate, andwollastonite can also be present in the composition.

The graft copolymers of this invention can be formed into usefularticles such as film and molded articles having improved surfaceproperties and oxygen barrier properties as well as improved thermalstability. The forming can be carried out by methods known in the artincluding, for example, thermoforming, injection molding, sheetextrusion, profile extrusion, and blow molding.

Isotactic index is defined as the per cent of olefin polymer insolublein xylene. The weight percent of olefin polymer soluble in xylene atroom temperature is determined by dissolving 2.5 g of the polymer in 250ml of xylene at room temperature in a vessel equipped with a stirrer,that is heated at 135° C. with agitation for 20 minutes. The solution iscooled to 25° C. while continuing the agitation, and then left to standwithout agitation for 30 minutes so that the solids can settle. Thesolids are filtered with filter paper, the remaining solution isevaporated by treating it with a nitrogen stream, and the solid residueis vacuum dried at 80° C. until a constant weight is reached. Thepercent by weight of polymer insoluble in xylene at room temperature isthe isotactic index of the polymer. The value obtained in this mannercorresponds substantially to the isotactic index determined viaextraction with boiling n-heptane, which by definition constitutes theisotactic index of the polymer.

Intrinsic viscosity is measured in decahydronaphthalene at 135° C.

Melt flow rate is measured according to ASTM D 1238 at 230° C. and 2.16kg.

The pore volume fraction values were determined by a mercury porosimetrytechnique in which the volume of mercury absorbed by the particles ismeasured. The volume of mercury absorbed corresponds to the volume ofthe pores. This method is described in Winslow, N. M. and Shapiro, J.J., “An Instrument for the Measurement of Pore-Size Distribution byMercury Penetration,” ASTM Bull., TP 49, 39-44 (February 1959), andRootare, H. M., “A Review of Mercury Porosimetry,” 225-252 (In Hirshhom,J. S. and Roll, K. H., Eds., Advanced Experimental Techniques in PowderMetallurgy, Plenum Press, New York, 1970).

The surface area measurements were made by the B.E.T. method asdescribed in JACS 60, 309 (1938).

In this specification, all parts and percentages are by weight unlessotherwise noted.

EXAMPLE 1

This example describes the preparation of a fluorinated graft copolymerusing a gaseous fluorinated monomer and a fluorinated solvent.

Polypropylene (500 g) having a melt flow rate (MFR) of 9 dg/min, a porevolume fraction of 0.28, a surface area of 0.3 m²/g, and greater than40% of the pores with a diameter greater than one micron, commerciallyavailable from Montell USA Inc., was charged into a 1 gallon highpressure stainless steel reactor. The reactor was fitted with nitrogeninlets and outlets, a vacuum outlet, two addition ports, and a helicalimpeller driven by compressed air. The reactor was equipped with ajacket through which hot or cold oil could be circulated. An inertatmosphere was established by repeated evacuation and purging withnitrogen. The bulk temperature was maintained at 23° C. After the finalevacuation, a suspension of di-(4-tert-butylcyclohexyl)peroxydicarbonate (10 g) in 100 g of deionized water was added to thepolypropylene under an inert atmosphere.2,2-Dichloro-1,1,1-trifluoroethane (200 ml) was introduced into thereactor after stirring for 10 minutes. The reactor was pressurized withvinylidene fluoride at 420 psi. Hot oil was circulated through thereactor jacket to raise the bulk temperature to 73° C. and to maintainthis temperature. The pressure of the reactor increased to around 520psi and vinylidene fluoride was fed on demand to maintain this pressure.After about 2 hours the temperature was raised to 100° C. and held atthis temperature for 30 minutes. The pressure was released, the reactorwas cooled down, and the polymer was discharged and dried for 4 hours inan air oven at 150° F. The amount of polyvinylidene fluorideincorporated into the graft copolymer was 9.4%.

EXAMPLE 2

This example describes the preparation of a graft copolymer comprising abackbone of propylene homopolymer, to which was grafted polyvinylidenefluoride. No fluorinated solvent was used.

The same polypropylene as used in Example 1 (500 g) was charged to thereactor and an inert atmosphere was established by repeated evacuationand purging with nitrogen at ˜15° C. After final evacuation, tert-butylperoctoate (12 g) and deionized water (50 g) were introduced into thereactor with stirring. After about 10 minutes of stirring, the reactorwas evacuated again and vinylidene fluoride was fed into the reactor at400 psi. The reactor was heated to 114° C. over a period of 30 minutesand maintained at this temperature for one hour. The pressure of thereactor was 880 psi. The reactor was cooled to room temperature (23°C.), the pressure was released, and the reactor was opened. The amountof polyvinylidene fluoride incorporated into the graft copolymer was 3.4wt. %.

EXAMPLE 3

This example describes the preparation of a graft copolymer comprising abackbone of propylene homopolymer, to which was grafted polyvinylidenefluoride.

Example 1 was repeated except that 2,2-dichloro-1,1,1-trifluoroethanewas added 30 minutes after the addition of thedi(4-tert-butylcyclohexyl)peroxy dicarbonate suspension, and the reactorwas pressurized to 260 psi with vinylidene fluoride. The amount ofpolyvinylidene fluoride incorporated into the graft copolymer was 10.1wt. %.

ATR infrared analysis of a plaque molded from the graft copolymerconfirmed that the graft-polymerized fluorine-containing monomer isfound at the surface of the plaque as well as on the inside.

EXAMPLE 4

This example describes the preparation of a graft copolymer comprising abackbone of propylene homopolymer, to which was grafted polyvinylidenefluoride.

After establishing an inert atmosphere as described in Example 1, asolution of tert-butyl peroxypivalate (6 g in 100 ml of pentane) wasadded to 550 g of the same polypropylene as used in Example 1 at ˜20° C.with stirring, and stirring was continued for 10 minutes. The reactorwas heated to 25° C. and pentane was removed by evacuating the reactor.The reactor was heated and 2,2-dichloro-1,1,1-trifluoroethane (200 ml)was introduced at 28° C. At 35° C. the reactor was pressurized withvinylidene fluoride to 240 psi. As the temperature increased to 90° C.over a period of 30 minutes, the pressure increased to 250 psi. Thetemperature and pressure were maintained for two hours. The temperatureof the reactor was then raised to 100° C. When that temperature wasreached, the pressure was released and the reactor was cooled to 30° C.The amount of polyvinylidene fluoride incorporated into the graftcopolymer was 17.5%.

EXAMPLE 5

This example describes the preparation of a graft copolymer comprising apropylene homopolymer backbone, to which was graft polymerizedpolyvinylidene fluoride.

The procedure of Example 1 was followed using the propylene homopolymerdescribed in Example 1. The peroxide was introduced at ˜19° C. andmixing was continued for 30 minutes. The reactor was subjected to vacuumand 2,2-dichloro-1,1,1-trifluoroethane was introduced. The reactorpressure was 20 psi. Vinylidene fluoride was fed into the reactor at 400psi and the reactor was heated to 85° C. over a period of 30 minutes,during which time the pressure increased to 630 psi. These conditionswere maintained for two hours. The temperature was raised to 90° C. andheld for 1 hour. The reactor was cooled to 30° C. and depressurized, andthe polymer was recovered. The amount of polyvinylidene fluorideincorporated into the graft copolymer was 17.5%.

EXAMPLE 6

This example describes the preparation of a graft copolymer comprising apropylene homopolymer backbone, to which was graft polymerizedpolyvinylidene fluoride.

The propylene homopolymer described in Example 1 was purged withnitrogen while heating to 70° C. The reactor was evacuated. A suspensionof di-(4-tert-butylcyclohexyl)peroxy dicarbonate in 100 g of deionizedwater was introduced and mixed for two minutes. The reactor wasevacuated again while maintaining a temperature of 70° C.2,2-Dichloro-1,1,1-trifluoroethane (200 ml) was introduced into thereactor while pressurizing with vinylidene fluoride at 480 psi. Thetemperature dropped to ˜53° C., after which the temperature was raisedto 85° C. and maintained for two hours. During this time period thepressure increased to 550 psi. The pressure was released and the reactorwas heated to 90° C. and held at this temperature for one hour. Thereactor was then cooled to 30° C. and the polymer was recovered. Theamount of polyvinylidene fluoride incorporated into the graft copolymerwas 15.7%.

EXAMPLE 7

This example describes the preparation of a graft copolymer comprising abackbone of propylene homopolymer to which was graft polymerizedpolyvinylidene fluoride. The starting material was peroxidized propylenehomopolymer.

The peroxidized propylene homopolymer was prepared by irradiatingpropylene homopolymer flake having a MFR of 0.4 dg/min, a pore volumefraction of 0.02 and a surface area of 0.03 m²/g, commercially availablefrom Montell USA Inc., in an inert atmosphere under an electron beam ata dose of 0.5 Mrad. The irradiated polymer was treated with 2.2% byvolume oxygen at 80° C. for 90 minutes and then at 140° C. for 60minutes. After the oxygen treatment, the polymer was treated at 140° C.for one hour in a nitrogen atmosphere and then cooled. The product had aperoxide concentration of 67 mmol/kg of polymer and a MFR of 890.

The peroxidized propylene homopolymer (800 g) was charged to the reactorand purged with nitrogen while heating. At 85° C.,2,2-dichloro-1,1,1-trifluoroethane (300 ml) was added and the reactorwas pressurized with vinylidene fluoride to 450 psi. The temperature ofthe reactor was raised to 120° C. and maintained for two hours. Thereactor pressure at this temperature was 620 psi. The pressure wasreleased and the reactor was cooled by cold oil circulation through thejacket while simultaneously purging with nitrogen. The amount ofpolyvinylidene fluoride incorporated into the graft copolymer was 20 wt%.

EXAMPLE 8

This example describes the preparation of a graft copolymer comprising abackbone of propylene homopolymer, to which was graft polymerizedvinylidene fluoride and methyl methacrylate (MMA). Peroxidized propylenehomopolymer was used as the starting material.

The peroxidized propylene homopolymer (800 g) described in Example 7 wascharged to the reactor and purged with nitrogen at room temperature for30 minutes, followed by purging while heating to 90° C. MMA (70 g) wascharged to the reactor and the mixture was stirred for five minutes.2,2-Dichloro-1,1,1-trifluoroethane (300 ml) was added to the reactor,followed by pressurizing with vinylidene fluoride to 220 psi. Thetemperature of the reactor was raised to 115°-120° C. and thistemperature was maintained for three hours. Vinylidene fluoride was fedon demand to maintain the reactor pressure at 260 psi. The pressure wasreleased and the reactor was cooled to 30° C. The amount ofpolyvinylidene fluoride incorporated into the graft copolymer was 9.5%and the amount of poly(methyl methacrylate) incorporated was 4.7%.

EXAMPLE 9

This example describes the preparation of a graft copolymer comprising abackbone of propylene homopolymer, to which was graft polymerizedvinylidene fluoride and MMA.

Di-(4-tert-butylcyclohexyl)peroxy dicarbonate (10 g as a 40% dispersionin water) diluted with 100 ml of deionized water was added to 500 g ofthe propylene homopolymer described in Example 1 under inert conditionsand mixed well at room temperature. 2,2-Dichloro-1,1,1-trifluoroethane(300 ml) and 90 g of MMA were introduced into the reactor. Vinylidenefluoride was fed at 320 psi. The temperature of the reactor was raisedto 90° C. over a period of about 30 minutes and this temperature wasmaintained for four hours. The pressure of the reactor increased to 560psi The pressure was released and the reactor was cooled to 30° C. Thepolymer product contained 12 wt. % poly(methyl methacrylate) and 3.6%polyvinylidene fluoride.

EXAMPLE 10

This example describes the preparation of a graft copolymer comprising apropylene homopolymer backbone, to which was graft polymerized2,2,3,4,4,4-hexafluorobutyl methacrylate.

The propylene described in Example 1 (400 g) was heated to 110° C. underinert conditions. Tertiary-butyl peroctoate (3.5 g, 50% solution inodorless mineral spirits) was diluted with 50 g odorless mineral spiritsand added to the reactor at the rate of 1 g/min.2,2,3,4,4,4-Hexafluorobutyl methacrylate (100 g) was diluted with 50 godorless mineral spirits and added continuously as a separate streamwith the peroxide at a rate of 2.24 g/min. The polymerization wascarried out at 110°-115° C. for two hours. The reactor was then heatedto 125° C. and subjected to vacuum to remove any unreacted monomer andodorless mineral spirits. The amount of polymerized monomer incorporatedinto the graft copolymer was 20 wt. %.

EXAMPLE 11

This example illustrates the thermal oxidative stability of graftcopolymers comprising a propylene homopolymer backbone, to which wasgrafted polyvinylidene fluoride (PVF2) or poly(vinylidenefluoride/methyl methacrylate) (PMMA/PVF2) produced under thepolymerization conditions shown in Table 1.

In each case the initiator was peroxidized propylene homopolymer(peroxidized PP), produced as described in Example 7. The solvent, whenpresent, was 2,2,dichloro-1,1,1-trifluoroethane. In Table 1, VF2 isvinylidene fluoride and MMA is methyl methacrylate. For the case wherethe grafting monomers were VF2/MMA, the vinylidene fluoride was fed ondemand to maintain the pressure, and the monomers were polymerizedsimultaneously. The starting materials for MMA/VF2(A) and MMA/VF2(B)were the same, except that a fluorinated solvent was used to prepareMMA/VF2(B) but not MMA/VF2(A).

TABLE 1 Amount Poly- Poly- of meri- meri- polymer- zation zation IzedMono- Temp. Time Pressure monomer mer Initiator (° C.) Solvent (hours)(psi) (wt. %) MMA/ Peroxidized 115 No 5 380 9.5% VF2(A) PVF₂ PP 4.7%PMMA MMA/ Peroxidized 115 Yes 3 260 9.5% VF2(B) PVF₂ PP 4.7% PMMA VF2Peroxidized 120 Yes 2 400  20% PP

The thermal oxidative stability of the samples was assessed bythermogravimetric analysis using a Perkin-Elmer TGA-7 analyzer. About 15mg of sample were scanned at 10°/min in air from 30° C. to 900° C. andthe weight loss was monitored. The results are shown in FIG. 1.

The data show that the graft copolymers made with fluorinated monomerswere more thermally stable than the propylene homopolymer alone. When afluorinated solvent is used, the same amount of polymerized fluorinatedmonomer can be incorporated into the graft copolymer using a lowerpressure and a shorter reaction time than when the solvent is notpresent.

Other features, advantages and embodiments of the invention disclosedherein will be readily apparent to those exercising ordinary skill afterreading the foregoing disclosures. In this regard, while specificembodiments of the invention have been described in considerable detail,variations and modifications of these embodiments can be effectedwithout departing from the spirit and scope of the invention asdescribed and claimed.

We claim:
 1. A process for preparing a fluorine-containing graftcopolymer comprising, in a non-oxidizing environment: (1) heating aperoxidized olefin polymer material to a temperature of about 60° toabout 140° C., (2) adding (a) at least one fluorinated gaseous monomerhaving the formula CR₁R₂═CR₃R₄, where R₁=H, F, or Cl; R₂=H, F, or Cl;R₃=H, F, CH₃, CF₃, or Cl, and R₄=H, F, or Cl, wherein at least twofluorine atoms are present, and, optionally, (b) at least onenon-fluorinated monomer selected from the group consisting of (i)vinyl-substituted aromatic, heterocyclic, and alicyclic compounds, (ii)unsaturated aliphatic nitriles, and (iii) unsaturated aliphaticmonocarboxylic acids or esters thereof, wherein the total amount ofmonomers added is about 1 to about 100 parts per hundred parts of theolefin polymer material, to produce and maintain a pressure of about 200to about 900 psi, (3) heating at a temperature within the rangespecified in step (1) for about 1 to about 6 hours, (4) cooling to roomtemperature, and (5) releasing the pressure to remove unreacted monomer.2. The process of claim 1 wherein the peroxidized olefin polymermaterial is selected from the group consisting of: (1) a peroxidizedhomopolymer of propylene having an isotactic index greater than 80; (2)a peroxidized copolymer of propylene and an olefin selected from thegroup consisting of ethylene and 4-10 C alpha-olefins, provided thatwhen the olefin is ethylene, the maximum polymerized ethylene content is10%, and when the olefin is a 4-10 C alpha-olefin, the maximumpolymerized content thereof is 20% by weight, the copolymer having anisotactic index greater than 85; (3) a peroxidized terpolymer ofpropylene and two olefins selected from the group consisting of ethyleneand 4-8 C alpha-olefins, provided that the maximum polymerized 4-8 Calpha-olefin content is 20% by weight, and, when ethylene is one of theolefins, the maximum polymerized ethylene content is 5% by weight, theterpolymer having an isotactic index greater than
 85. 3. The process ofclaim 1 wherein the fluorinated monomer is vinylidene fluoride.
 4. Theprocess of claim 1 wherein the non-fluorinated monomer is methylmethacrylate.
 5. A fluorine-containing graft copolymer comprising aparticulate olefin polymer material having a backbone to which is graftpolymerized (a) at least one fluorinated monomer having the formulaCH₂═C(R₁)—(COOR₂), where R₁=H, CH₃, or CF₃, and R₂ is H or a partiallyor completely fluorinated C₁-C₁₂ alkyl group, and, optionally, (b) atleast one non-fluorinated monomer selected from the group consisting of(i) vinyl-substituted aromatic, heterocyclic, and alicyclic compounds,(ii) unsaturated aliphatic nitriles, and (iii) unsaturated aliphaticmonocarboxylic acids or esters thereof, wherein the total amount ofmonomers added is about 1 to about 120 parts per hundred parts of theolefin polymer material and the fluorine-containing graft copolymer ismade by a process comprising, in a non-oxidizing environment: (1)heating a peroxidized olefin polymer material to a temperature of about60° to about 140° C., (2) adding (a) at least one fluorinated gaseousmonomer having the formula CR₁,R₂═CR₃R₄, where R₁=H, F, or Cl; R₂=H, F,or Cl; R₃=H, F, CH₃, CF₃, or Cl, and R₄=H, F, or Cl, wherein at leasttwo fluorine atoms are present, and, optionally, (b) at least onenon-fluorinated monomer selected from the group consisting of (i)vinyl-substituted aromatic, heterocyclic, and alicyclic compounds, (ii)unsaturated aliphatic nitriles, and (iii) unsaturated aliphaticmonocarboxylic acids or esters thereof, wherein the total amount ofmonomers added is about 1 to about 100 parts per hundred parts of theolefin polymer material, to produce and maintain a pressure of about 200to about 900 psi, (3) heating at a temperature within the rangespecified in step (1) for about 1 to about 6 hours, (4) cooling to roomtemperature, and (5) releasing the pressure to remove unreacted monomer.6. The graft copolymer of claim 5 wherein the particulate olefin polymermaterial is selected from the group consisting of: (1) a homopolymer ofpropylene having an isotactic index greater than 80; (2) a copolymer ofpropylene and an olefin selected from the group consisting of ethyleneand 4-10 C alpha-olefins, provided that when the olefin is ethylene, themaximum polymerized ethylene content is 10%, and, when the olefin is a4-10 C alpha-olefin, the maximum polymerized content thereof is 20% byweight, the copolymer having an isotactic index greater than 85; (3) aterpolymer of propylene and two olefins selected from the groupconsisting of ethylene and 4-8 C alpha-olefins, provided that themaximum polymerized 4-8 C alpha-olefin content is 20% by weight, and,when ethylene is one of the olefins, the maximum polymerized ethylenecontent is 5% by weight, the terpolymer having an isotactic indexgreater than 85; (4) an olefin polymer composition comprising: (a) about10% to about 60% by weight of a propylene homopolymer having anisotactic index greater than 80, or a copolymer of monomers selectedfrom the group consisting of (i) propylene and ethylene, (ii) propylene,ethylene and a 4-8 C alpha-olefin, and (iii) propylene and a 4-8 Calpha-olefin, the copolymer having a polymerized propylene content ofmore than 85% by weight and an isotactic index greater than 85; (b)about 5% to about 25% by weight of a copolymer of ethylene and propyleneor a 4-8 C alpha-olefin that is insoluble in xylene at ambienttemperature; and (c) about 30% to about 70% by weight of an elastomericcopolymer of monomers selected from the group consisting of (i) ethyleneand propylene, (ii) ethylene, propylene, and a 4-8 C alpha-olefin, and(iii) ethylene and a 4-8 C alpha-olefin, the copolymer optionallycontaining about 0.5% to about 10% by weight of a polymerized diene andcontaining less than 70% by weight of polymerized ethylene and beingsoluble in xylene at ambient temperature and having an intrinsicviscosity, measured in decahydronaphthalene at 135° C., of about 1.5 toabout 4.0 dl/g, wherein the total amount of (b) and (c), based on thetotal olefin polymer composition, is about 50% to about 90%, the weightratio of (b)/(c) is less than 0.4, and the composition is prepared bypolymerization in at least two stages and has a flexural modulus of lessthan 150 MPa; and (5) a thermoplastic olefin comprising: (a) about 10%to about 60% of a propylene homopolymer having an isotactic indexgreater than 80, or a copolymer of monomers selected from the groupconsisting of (i) ethylene and propylene, (ii) ethylene, propylene and a4-8 C alpha-olefin, and (iii) ethylene and a 4-8 C alpha-olefin, thecopolymer having a polymerized propylene content greater than 85% and anisotactic index of greater than 85; (b) about 20% to about 60% of anamorphous copolymer from monomers selected from the group consisting of(i) ethylene and propylene, (ii) ethylene, propylene, and a 4-8 Calpha-olefin, and (iii) ethylene and a 4-8 C alpha-olefin, the copolymeroptionally containing about 0.5% to about 10% of a polymerized diene,and containing less than 70% polymerized ethylene and being soluble inxylene at ambient temperature; and (c) about 3% to about 40% of acopolymer of ethylene and propylene or a 4-8 C alpha-olefin that isinsoluble in xylene at ambient temperature, wherein the thermoplasticolefin has a flexural modulus of greater than 150 but less than 1200MPa.
 7. The graft copolymer of claim 5 wherein the fluorinated monomeris 2,2,3,4,4,4-hexafluorobutyl methacrylate.
 8. A process for preparinga fluorine-containing graft copolymer comprising, in a non-oxidizingenvironment: (1) treating a particulate olefin polymer material at atemperature of 60° C. to 125° C. with about 0.1 to about 6.0 parts perhundred parts of the olefin polymer material, of an organic compoundthat is a chemical free radical polymerization initiator and has adecomposition half-life at the temperature used of about 1 to about 240minutes; (2) treating the olefin polymer material at the temperatureselected over a time period that coincides with or follows (1), with orwithout overlap, with (a) at least one fluorinated monomer having theformula CH₂═C(R₁)—(COOR₂), where R₁=H, CH₃, or CF₃, and R₂ is H or apartially or completely fluorinated C₁-C₁₂ alkyl group, and, optionally,(b) at least one non-fluorinated monomer selected from the groupconsisting of (i) vinyl-substituted aromatic, heterocyclic, andalicyclic compounds, (ii) unsaturated aliphatic nitriles, and (iii)unsaturated aliphatic monocarboxylic acids or esters thereof, whereinthe total amount of monomers added is about 1 to about 120 parts perhundred parts of the olefin polymer material, the monomer being added tothe olefin polymer material over a time period from 5 minutes to 3-4hours to provide a rate of addition that is less than about 4.5 pph perminute at any addition level; and thereafter (3) simultaneously orsuccessively, in any order, removing any unreacted monomer from theresulting grafted particulate olefin polymer material, and decomposingany unreacted initiator and deactivating any residual free radicals inthe material.
 9. The process of claim 8 wherein the particulate olefinpolymer material is selected from the group consisting of: (1) ahomopolymer of propylene having an isotactic index greater than 80; (2)a copolymer of propylene and an olefin selected from the groupconsisting of ethylene and 4-10 C alpha-olefins, provided that when theolefin is ethylene, the maximum polymerized ethylene content is 10% andwhen the olefin is a 4-10 C alpha-olefin, the maximum polymerizedcontent thereof is 20% by weight, the copolymer having an isotacticindex greater than 85; (3) a terpolymer of propylene and two olefinsselected from the group consisting of ethylene and 4-8 C alpha-olefins,provided that the maximum polymerized 4-8 C alpha-olefin content is 20%by weight, and, when ethylene is one of the olefins, the maximumpolymerized ethylene content is 5% by weight, the terpolymer having anisotactic index greater than 85; (4) an olefin polymer compositioncomprising: (a) about 10% to about 60% by weight of a propylenehomopolymer having an isotactic index greater than 80 or a copolymer ofmonomers selected from the group consisting of (i) propylene andethylene, (ii) propylene, ethylene and a 4-8 C alpha-olefin, and (iii)propylene and a 4-8 C alpha-olefin, the copolymer having a polymerizedpropylene content of more than 85% by weight and an isotactic indexgreater than 85; (b) about 5% to about 25% by weight of a copolymer ofethylene and propylene or a 4-8 C alpha-olefin that is insoluble inxylene at ambient temperature; and (c) about 30% to about 70% by weightof an elastomeric copolymer of monomers selected from the groupconsisting of (i) ethylene and propylene, (ii) ethylene, propylene, anda 4-8 C alpha-olefin, and (iii) ethylene and a 4-8 C alpha-olefin, thecopolymer optionally containing about 0.5% to about 10% by weight of apolymerized diene and containing less than 70% by weight of polymerizedethylene and being soluble in xylene at ambient temperature and havingan intrinsic viscosity, measured in decahydronaphthalene at 135° C., ofabout 1.5 to about 4.0 dl/g, wherein the total amount of (b) and (c),based on the total olefin polymer composition, is about 50% to about90%, the weight ratio of (b)/(c) is less than 0.4, and the compositionis prepared by polymerization in at least two stages and has a flexuralmodulus of less than 150 MPa; and (5) a thermoplastic olefin comprising:(a) about 10% to about 60% of a propylene homopolymer having anisotactic index greater than 80, or a copolymer of monomers selectedfrom the group consisting of (i) ethylene and propylene, (ii) ethylene,propylene and a 4-8 C alpha-olefin, and (iii) ethylene and a 4-8 Calpha-olefin, the copolymer having a polymerized propylene contentgreater than 85% and an isotactic index of greater than 85; (b) about20% to about 60% of an amorphous copolymer from monomers selected fromthe group consisting of (i) ethylene and propylene, (ii) ethylene,propylene, and a 4-8 C alpha-olefin, and (iii) ethylene and a 4-8 Calpha-olefin, the copolymer optionally containing about 0.5% to about10% of a polymerized diene, and containing less than 70% polymerizedethylene and being soluble in xylene at ambient temperature; and (c)about 3% to about 40% of a copolymer of ethylene and propylene or a 4-8C alpha-olefin that is insoluble in xylene at ambient temperature,wherein the thermoplastic olefin has a flexural modulus of greater than150 but less than 1200 MP.
 10. The process of claim 8 wherein thefluorinated monomer is 2,2,3,4,4,4-hexafluorobutyl methacrylate.
 11. Afluorine-containing graft copolymer comprising a particulate olefinpolymer material having a backbone to which is graft polymerized (a) atleast one fluorinated monomer having the formula CH₂═C(R₁)—(COOR₂),where R₁=H, CH₃, or CF₃, and R₂ is H or a partially or completelyfluorinated C₁-C₁₂ alkyl group, and, optionally, (b) at least onenon-fluorinated monomer selected from the group consisting of (i)vinyl-substituted aromatic, heterocyclic, and alicyclic compounds, (ii)unsaturated aliphatic nitriles, and (iii) unsaturated aliphaticmonocarboxylic acids or esters thereof, wherein the total amount ofmonomers added is about 1 to about 120 parts per hundred parts of theolefin polymer material and the fluorine-containing graft copolymer ismade by a process comprising, in a non-oxidizing environment: (1)treating a particulate olefin polymer material at a temperature of 60°C. to 125° C. with about 0.1 to about 6.0 parts per hundred parts of theolefin polymer material, of an organic compound that is a chemical freeradical polymerization initiator and has a decomposition half-life atthe temperature used of about 1 to about 240 minutes; (2) treating theolefin polymer material at the temperature selected over a time periodthat coincides with or follows (1), with or without overlap, with (a) atleast one fluorinated monomer having the formula CH₂═C(R₁)—(COOR₂),where R₁=H, CH₃, or CF₅, and R₂ is H or a partially or completelyfluorinated C₁-C₁₂ alkyl group, and, optionally, (b) at least onenon-fluorinated monomer selected from the group consisting of (i)vinyl-substituted aromatic, heterocyclic, and alicyclic compounds, (ii)unsaturated aliphatic nitriles, and (iii) unsaturated aliphaticmonocarboxylic acids or esters thereof, wherein the total amount ofmonomers added is about 1 to about 120 parts per hundred parts of theolefin polymer material, the monomer being added to the olefin polymermaterial over a time period from 5 minutes to 3-4 hours to provide arate of addition that is less than about 4.5 pph per minute at anyaddition level; and thereafter (3) simultaneously or successively, inany order, removing any unreacted monomer from the resulting graftedparticulate olefin polymer material, and decomposing any unreactedinitiator and deactivating any residual free radicals in the material.